US6013151A - High speed method of making microporous film products - Google Patents

High speed method of making microporous film products Download PDF

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Publication number
US6013151A
US6013151A US09/080,063 US8006398A US6013151A US 6013151 A US6013151 A US 6013151A US 8006398 A US8006398 A US 8006398A US 6013151 A US6013151 A US 6013151A
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US
United States
Prior art keywords
film
weight
high speed
speed method
styrene
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US09/080,063
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English (en)
Inventor
Pai-Chuan Wu
Leopoldo V. Cancio
Girish K. Sharma
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Berry Film Products Co Inc
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Clopay Plastic Products Co Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Application filed by Clopay Plastic Products Co Inc filed Critical Clopay Plastic Products Co Inc
Assigned to CLOPAY PLASTIC PRODUCTS COMPANY, INC. reassignment CLOPAY PLASTIC PRODUCTS COMPANY, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CANCIO, LEOPOLDO V., SHARMA, GIRISH K., WU, PAI-CHUAN
Priority to US09/080,063 priority Critical patent/US6013151A/en
Priority to ARP990102208A priority patent/AR015777A1/es
Priority to TW088107700A priority patent/TWI239978B/zh
Priority to TW094108528A priority patent/TWI252858B/zh
Priority to EP99923008A priority patent/EP1078013B1/de
Priority to PL343906A priority patent/PL201500B1/pl
Priority to RU2000128113/04A priority patent/RU2224772C2/ru
Priority to EP04077292A priority patent/EP1482005A3/de
Priority to KR1020007012175A priority patent/KR100583548B1/ko
Priority to ES99923008T priority patent/ES2244195T3/es
Priority to NZ507461A priority patent/NZ507461A/en
Priority to CA002329529A priority patent/CA2329529A1/en
Priority to BR9910040-1A priority patent/BR9910040A/pt
Priority to JP2000549665A priority patent/JP2002515367A/ja
Priority to HU0102654A priority patent/HU226496B1/hu
Priority to KR1020067001225A priority patent/KR100704513B1/ko
Priority to PCT/US1999/010562 priority patent/WO1999060050A1/en
Priority to AU39877/99A priority patent/AU739260B2/en
Priority to CZ20004041A priority patent/CZ298026B6/cs
Priority to AT99923008T priority patent/ATE301154T1/de
Priority to DE69926497T priority patent/DE69926497T2/de
Priority to CN99805984A priority patent/CN1300305A/zh
Priority to US09/480,374 priority patent/US6656581B2/en
Publication of US6013151A publication Critical patent/US6013151A/en
Application granted granted Critical
Priority to US09/548,403 priority patent/US20030047271A1/en
Priority to NO20005689A priority patent/NO20005689D0/no
Assigned to JP MORGAN CHASE BANK, N.A. reassignment JP MORGAN CHASE BANK, N.A. SECURITY AGREEMENT Assignors: CLOPAY PLASTIC PRODUCTS COMPANY, INC.
Assigned to JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT reassignment JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT AMENDED AND RESTATED GRANT OF SECURITY INTEREST IN PATENT RIGHTS Assignors: CLOPAY PLASTIC PRODUCTS COMPANY, INC.
Assigned to GOLDMAN SACHS LENDING PARTNERS, LLC AS COLLATERAL AGENT reassignment GOLDMAN SACHS LENDING PARTNERS, LLC AS COLLATERAL AGENT SECURITY AGREEMENT Assignors: AMES TRUE TEMPER, INC., CLOPAY BUILDING PRODUCTS COMPANY, INC., CLOPAY PLASTIC PRODUCTS COMPANY, INC.
Assigned to CLOPAY PLASTIC PRODUCTS COMPANY, INC. reassignment CLOPAY PLASTIC PRODUCTS COMPANY, INC. RELEASE BY SECURED PARTY (SEE DOCUMENT FOR DETAILS). Assignors: GOLDMAN SACHS LENDING PARTNERS LLC
Assigned to CLOPAY PLASTIC PRODUCTS COMPANY, INC. reassignment CLOPAY PLASTIC PRODUCTS COMPANY, INC. TERMINATION AND RELEASE OF SECURITY INTEREST IN PATENT RIGHTS Assignors: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
Assigned to JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT reassignment JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT SECURITY AGREEMENT Assignors: CLOPAY PLASTIC PRODUCTS COMPANY, INC.
Assigned to CLOPAY PLASTIC PRODUCTS COMPANY, INC. reassignment CLOPAY PLASTIC PRODUCTS COMPANY, INC. RELEASE BY SECURED PARTY (SEE DOCUMENT FOR DETAILS). Assignors: JPMORGAN CHASE BANK, N.A.
Assigned to CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, BANK OF AMERICA, N.A., reassignment CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CLOPAY PLASTIC PRODUCTS COMPANY, INC.
Assigned to U.S. BANK NATIONAL ASSOCIATION reassignment U.S. BANK NATIONAL ASSOCIATION SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CLOPAY PLASTIC PRODUCTS COMPANY, INC.
Assigned to BERRY FILM PRODUCTS COMPANY, INC. reassignment BERRY FILM PRODUCTS COMPANY, INC. CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: CLOPAY PLASTIC PRODUCTS COMPANY, INC.
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/12—Layered products comprising a layer of synthetic resin next to a fibrous or filamentary layer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C55/00—Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/02—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets
    • B29C55/04—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets uniaxial, e.g. oblique
    • B29C55/06—Shaping by stretching, e.g. drawing through a die; Apparatus therefor of plates or sheets uniaxial, e.g. oblique parallel with the direction of feed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C67/00—Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00
    • B29C67/20—Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00 for porous or cellular articles, e.g. of foam plastics, coarse-pored
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
    • B32B27/20—Layered products comprising a layer of synthetic resin characterised by the use of special additives using fillers, pigments, thixotroping agents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B5/00—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts
    • B32B5/02—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by structural features of a fibrous or filamentary layer
    • B32B5/022—Non-woven fabric
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18—Manufacture of films or sheets
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24—Acids; Salts thereof
    • C08K3/26—Carbonates; Bicarbonates
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04—Homopolymers or copolymers of ethene
    • C08L23/08—Copolymers of ethene
    • C08L23/0807—Copolymers of ethene with unsaturated hydrocarbons only containing more than three carbon atoms
    • C08L23/0815—Copolymers of ethene with aliphatic 1-olefins
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04—Polymers of ethylene
    • B29K2023/06—PE, i.e. polyethylene
    • B29K2023/0608—PE, i.e. polyethylene characterised by its density
    • B29K2023/0625—LLDPE, i.e. linear low density polyethylene
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04—Polymers of ethylene
    • B29K2023/08—Copolymers of ethylene
    • B29K2023/083—EVA, i.e. ethylene vinyl acetate copolymer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/04—Condition, form or state of moulded material or of the material to be shaped cellular or porous
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2250/00—Layers arrangement
    • B32B2250/24—All layers being polymeric
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2262/00—Composition or structural features of fibres which form a fibrous or filamentary layer or are present as additives
    • B32B2262/02—Synthetic macromolecular fibres
    • B32B2262/0253—Polyolefin fibres
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2262/00—Composition or structural features of fibres which form a fibrous or filamentary layer or are present as additives
    • B32B2262/02—Synthetic macromolecular fibres
    • B32B2262/0261—Polyamide fibres
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2262/00—Composition or structural features of fibres which form a fibrous or filamentary layer or are present as additives
    • B32B2262/02—Synthetic macromolecular fibres
    • B32B2262/0276—Polyester fibres
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2270/00—Resin or rubber layer containing a blend of at least two different polymers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2305/00—Condition, form or state of the layers or laminate
    • B32B2305/02—Cellular or porous
    • B32B2305/026—Porous
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00—Properties of the layers or laminate
    • B32B2307/70—Other properties
    • B32B2307/726—Permeability to liquids, absorption
    • B32B2307/7265—Non-permeable
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/04—Homopolymers or copolymers of ethene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/04—Homopolymers or copolymers of ethene
    • C08J2323/06—Polyethene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24—Acids; Salts thereof
    • C08K3/26—Carbonates; Bicarbonates
    • C08K2003/265—Calcium, strontium or barium carbonate
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04—Homopolymers or copolymers of ethene
    • C08L23/06—Polyethene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L53/00—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C08L53/02—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers of vinyl-aromatic monomers and conjugated dienes

Definitions

  • U.S. Pat. No. 3,832,267 to Liu, teaches the melt-embossing of a polyolefin film containing a dispersed amorphous polymer phase prior to stretching or orientation to improve gas and moisture vapor transmission of the film.
  • a film of crystalline polypropylene having a dispersed amorphous polypropylene phase is first embossed prior to biaxially drawing (stretching) to produce an oriented imperforate film having greater permeability.
  • the dispersed amorphous phase serves to provide microvoids to enhance the permeability of the otherwise imperforate film to improve moisture vapor transmission (MVT).
  • the embossed film is preferably embossed and drawn sequentially.
  • EP patent 141592 discloses the use of a polyolefin, particularly ethylene vinyl acetate (EVA) containing a dispersed polystyrene phase which, when stretched, produces a voided film which improves the moisture vapor permeability of the film.
  • EVA ethylene vinyl acetate
  • This EP '592 patent also discloses the sequential steps of embossing the EVA film with thick and thin areas followed by stretching to first provide a film having voids which, when further stretched, produces a net-like product.
  • 4,452,845 and 4,596,738 also disclose stretched thermoplastic films where the dispersed phase may be a polyethylene filled with calcium carbonate to provide the microvoids upon stretching.
  • U.S. Pat. Nos. 4,777,073; 4,814,124; and 4,921,653 disclose the same processes described by the above-mentioned earlier publications involving the steps of first embossing a polyolefin film containing a filler and then stretching that film to provide a microporous product.
  • microporous films have been produced from a blend of linear low density polyethylene (LLDPE) and low density polyethylene (LDPE) with barium sulfate as the inorganic filler having an average particle diameter of 0.1-7 microns. It is also known to modify blends of LLDPE and LDPE with a thermoplastic rubber such as Kraton.
  • Other patents, such as U.S. Pat. No. 4,582,871, disclose the use of thermoplastic styrene block tripolymers in the production of microporous films with other incompatible polymers such as styrene.
  • extrusion lamination of unstretched nonwoven webs include U.S. Pat. Nos. 2,714,571; 3,058,868; 4,522,203; 4,614,679; 4,692,368; 4,753,840 and 5,035,941.
  • the above '863 and '368 patents disclose stretching extruded polymeric films prior to laminating with unstretched nonwoven fibrous webs at pressure roller nips.
  • the '203 and '941 patents are directed to co-extruding multiple polymeric films with unstretched nonwoven webs at pressure roller nips.
  • the '840 patent discloses preforming nonwoven polymeric fiber materials prior to extrusion laminating with films to improve bonding between the nonwoven fibers and films.
  • the '840 patent discloses conventional embossing techniques to form densified and undensified areas in nonwoven base plies prior to extrusion lamination to improve bonding between nonwoven fibrous webs and films by means of the densified fiber areas.
  • the '941 patent also teaches that unstretched nonwoven webs that are extrusion laminated to single ply polymeric films are susceptible to pinholes caused by fibers extending generally vertically from the plane of the fiber substrate and, accordingly, this patent discloses using multiple co-extruded film plies to prevent pinhole problems.
  • methods for bonding loose nonwoven fibers to polymeric film are disclosed in U.S. Pat. Nos. 3,622,422; 4,379,197 and 4,725,473.
  • Efforts have also been made to make breathable non-woven composite barrier fabrics which are impervious to liquids, but which are permeable to water vapor.
  • U.S. Pat. No. 5,409,761 is an example of a fabrication process from the patent art. According to this '761 patent, a nonwoven composite fabric is made by ultrasonically bonding a microporous thermoplastic film to a layer of nonwoven fibrous thermoplastic material.
  • This invention is directed to a high speed method of making a microporous thermoplastic film.
  • the microporous film is permeable to air and water vapor, but is a barrier to liquid. Breathable laminates of microporous film with nonwoven substrates are also produced at high speeds according to the method of this invention.
  • the high speed method of this invention involves melt-blending a composition comprising
  • the melt-blended composition is extruded, preferably through a slot die, into a nip of rollers with an air knife to form a film at a speed on the order of at least about 550 fpm to about 1200 fpm without draw resonance. Speeds of at least about 750 fpm to about 1200 fpm, or greater, have been achieved without draw resonance.
  • the use of the air knife to assist in the elimination of draw resonance is known, for example, by reference to U.S. Pat. No. 4,626,574. Thereafter, an incremental stretching force is applied to the film at the high speeds along lines substantially uniformally across the film and throughout its depth to provide a microporous film.
  • this invention provides a high speed method of making microporous films and laminates with nonwoven substrates of uniform gauge.
  • the problem of draw resonance which has heretofore resulted in irregular gauge or thickness in the film products is avoided, even though line speeds of about 750-1200 fpm are achieved.
  • the blend of LLDPE and LDPE within the approximate ranges of components enables the production of film without breakage and pin holes when balanced with the prescribed amount of calcium carbonate.
  • the LLDPE is present in an amount of about 35% to about 45% by weight in order to provide a sufficient amount of matrix to carry the calcium carbonate filler particles thereby enabling the film to be handled and stretched without pin holing and breakage.
  • the LDPE in an amount of about 3% to about 10% by weight also contributes to the production of film without pin holing and enables the high speed production without draw resonance.
  • the polymeric matrix is balanced with an amount of about 40% to about 55% by weight of calcium carbonate particles having an average particle diameter of preferably about 1 micron to achieve sufficient MVT in the range of about 1000 gms/m 2 /day to 4000 gms/m 2 /day.
  • the melt-blended composition requires a triblock polymer in an amount of about 2% to about 6% by weight to facilitate stretching in high-speed production without breakage.
  • An incremental stretching force is applied inline to the formed film under ambient conditions or at an elevated temperature at speeds of at least about 550 fpm to about 1200 fpm, or more, along lines substantially uniformly across the film and throughout it depth to provide a microporous film.
  • the method of this invention also involves lamination of the microporous-formable thermoplastic film to a nonwoven fibrous web during extrusion.
  • the extrusion lamination is conducted at the same high speeds where a nonwoven fibrous web is introduced into the nip of rollers along with the microporous-formable thermoplastic extrudate.
  • the compressive force between the fibrous web and the extrudate is controlled to bond one surface of the web to the film and form a laminate.
  • the laminate is then incrementally stretched along lines substantially uniformly across the laminate and throughout its depth in one direction to render the film microporous.
  • the laminate may be stretched in both the cross direction and the machine direction to provide breathable cloth-like liquid barriers capable of transmitting moisture vapor and air.
  • microporous film and laminated products thereof with nonwoven fibrous webs on high-speed production machinery. It is the further objective of the method to produce such microporous film products of regular gauge, uniform porosity and without breakage.
  • the melt-blended composition consists essentially of about 42% by weight LLDPE, about 4% by weight LDPE, about 44% by weight calcium carbonate filler particles having an average particle size of about 1 micron, and about 3% by weight triblock polymer, especially styrene-butadiene-styrene.
  • the stiffness properties of the microporous film products may be controlled by including high density polyethylene on the order of about 0-5% by weight and including 0-4% by weight titanium dioxide.
  • processing aid such as a flurocarbon polymer in an amount of about 0.1% to about 0.2% by weight is added, as exemplified by 1-propene,1,1,2,3,3,3-hexafluoro copolymer with 1,1-difluoroethylene.
  • the triblock polymer may also be blended with oil, hydrocarbon, antioxidant and stabilizer.
  • Antioxidants include tetrakis (methylene(3,5-di-tert-butyl-4-hydroxyhydrocinnamate))methane (trade name is Irganox 1010), and tris(2,4-di-tert-butylphenyl)phosphite (trade name is Irgafos 168) at a total of 500-4000 ppm (parts per million).
  • embossed and flat films may be produced according to the principles of this invention.
  • the nip of rollers comprises a metal embossing roller and a rubber roller.
  • the compressive force between the rollers forms an embossed film of desired thickness on the order of about 0.5 to about 10 mils.
  • rollers which provide a polished chrome surface form a flat film.
  • microporous film products are produced having high moisture vapor transmission rate (MVTR) within the acceptable range of about 1000 to 4000 gms/m 2 /day.
  • MVTR moisture vapor transmission rate
  • flat film can be incrementally stretched more uniformly than embossed film.
  • the process may be conducted at ambient or room temperature or at elevated temperatures. As described above, laminates of the microporous film may be obtained with nonwoven fibrous webs.
  • the nonwoven fibrous web may comprise fibers of polyethylene, polypropylene, polyesters, rayon, cellulose, nylon, and blends of such fibers.
  • the fibers are usually staple fibers or continuous filaments.
  • the nonwovens are usually referred to as spunbond, carded, meltblown, and the like.
  • the fibers or filaments may be bicomponent to facilitate bonding.
  • a fiber having a sheath and core of different polymers such as polyethylene (PE) and polypropylene (PP) may be used; or mixtures of PE and PP fibers may be used.
  • nonwoven fibrous web is used in its generic sense to define a generally planar structure that is relatively flat, flexible and porous, and is composed of staple fibers or continuous filaments.
  • nonwovens see "Nonwoven Fabric Primer and Reference Sampler” by E. A. Vaughn, Association of the Nonwoven Fabrics Industry, 3d Edition (1992).
  • the microporous laminate employs a film having a gauge or a thickness between about 0.25 and 10 mils and, depending upon use, the film thickness will vary and, most preferably, in disposable applications is the order of about 0.25 to 2 mils in thickness.
  • the nonwoven fibrous webs of the laminated sheet normally have a weight of about 5 gms/yd 2 to 75 gms/yd 2 , preferably about 20 to about 40 gms/yd 2 .
  • the composite or laminate can be incrementally stretched in the cross direction (CD) to form a CD stretched composite. Furthermore, CD stretching may be followed by stretching in the machine direction (MD) to form a composite which is stretched in both CD and MD directions.
  • the microporous film or laminate may be used in many different applications such as baby diapers, baby training pants, catamenial pads and garments, and the like where moisture vapor and air transmission properties, as well as fluid barrier properties, are needed.
  • stretchers and techniques may be employed to stretch the film or laminate of a nonwoven fibrous web and microporous-formable film. These laminates of nonwoven carded fibrous webs of staple fibers or nonwoven spun-bonded fibrous webs may be stretched with the stretchers and techniques described as follows:
  • the diagonal intermeshing stretcher consists of a pair of left hand and right hand helical gear-like elements on parallel shafts.
  • the shafts are disposed between two machine side plates, the lower shaft being located in fixed bearings and the upper shaft being located in bearings in vertically slidable members.
  • the slidable members are adjustable in the vertical direction by wedge shaped elements operable by adjusting screws. Screwing the wedges out or in will move the vertically slidable member respectively down or up to further engage or disengage the gear-like teeth of the upper intermeshing roll with the lower intermeshing roll.
  • Micrometers mounted to the side frames are operable to indicate the depth of engagement of the teeth of the intermeshing roll.
  • Air cylinders are employed to hold the slidable members in their lower engaged position firmly against the adjusting wedges to oppose the upward force exerted by the material being stretched. These cylinders may also be retracted to disengage the upper and lower intermeshing rolls from each other for purposes of threading material through the intermeshing equipment or in conjunction with a safety circuit which would open all the machine nip points when activated.
  • a drive means is typically utilized to drive the stationery intermeshing roll. If the upper intermeshing roll is to be disengageable for purposes of machine threading or safety, it is preferable to use an antibacklash gearing arrangement between the upper and lower intermeshing rolls to assure that upon reengagement the teeth of one intermeshing roll always fall between the teeth of the other intermeshing roll and potentially damaging physical contact between addenda of intermeshing teeth is avoided. If the intermeshing rolls are to remain in constant engagement, the upper intermeshing roll typically need not be driven. Drive may be accomplished by the driven intermeshing roll through the material being stretched.
  • the intermeshing rolls closely resemble fine pitch helical gears.
  • the rolls have 5.935" diameter, 45° helix angle, a 0.100" normal pitch, 30 diametral pitch, 141/2° pressure angle, and are basically a long addendum topped gear. This produces a narrow, deep tooth profile which allows up to about 0.090" of intermeshing engagement and about 0.005" clearance on the sides of the tooth for material thickness.
  • the teeth are not designed to transmit rotational torque and do not contact metal-to-metal in normal intermeshing stretching operation.
  • the CD intermeshing stretching equipment is identical to the diagonal intermeshing stretcher with differences in the design of the intermeshing rolls and other minor areas noted below. Since the CD intermeshing elements are capable of large engagement depths, it is important that the equipment incorporate a means of causing the shafts of the two intermeshing rolls to remain parallel when the top shaft is raising or lowering. This is necessary to assure that the teeth of one intermeshing roll always fall between the teeth of the other intermeshing roll and potentially damaging physical contact between intermeshing teeth is avoided.
  • This parallel motion is assured by a rack and gear arrangement wherein a stationary gear rack is attached to each side frame in juxtaposition to the vertically slidable members. A shaft traverses the side frames and operates in a bearing in each of the vertically slidable members. A gear resides on each end of this shaft and operates in engagement with the racks to produce the desired parallel motion.
  • the drive for the CD intermeshing stretcher must operate both upper and lower intermeshing rolls except in the case of intermeshing stretching of materials with a relatively high coefficient of friction.
  • the drive need not be antibacklash, however, because a small amount of machine direction misalignment or drive slippage will cause no problem. The reason for this will become evident with a description of the CD intermeshing elements.
  • the CD intermeshing elements are machined from solid material but can best be described as an alternating stack of two different diameter disks.
  • the intermeshing disks would be 6" in diameter, 0.031" thick, and have a full radius on their edge.
  • the spacer disks separating the intermeshing disks would be 51/2" in diameter and 0.069" in thickness. Two rolls of this configuration would be able to be intermeshed up to 0.231" leaving 0.019" clearance for material on all sides.
  • this CD intermeshing element configuration would have a 0.100" pitch.
  • the MD intermeshing stretching equipment is identical to the diagonal intermeshing stretch except for the design of the intermeshing rolls.
  • the MD intermeshing rolls closely resemble fine pitch spur gears.
  • the rolls have a 5.933" diameter, 0.100" pitch, 30 Diametral pitch, 141/2° pressure angle, and are basically a long addendum, topped gear.
  • a second pass was taken on these rolls with the gear hob offset 0.010" to provide a narrowed tooth with more clearance. With about 0.090" of engagement, this configuration will have about 0.010" clearance on the sides for material thickness.
  • the above described diagonal, CD or MD intermeshing stretchers may be employed to produce the incrementally stretched film or laminate of nonwoven fibrous web and microporous-formable film to form the microporous film products of this invention.
  • the stretching operation may be employed on an extrusion laminate of a nonwoven fibrous web of staple fibers or spun-bonded filaments and microporous-formable thermoplastic film.
  • a laminate of a nonwoven fibrous web of spun-bonded filaments may be incrementally stretched to provide a very soft fibrous finish to the laminate that looks like cloth.
  • the laminate of nonwoven fibrous web and microporous-formable film is incrementally stretched using, for instance, the CD and/or MD intermeshing stretcher with one pass through the stretcher with a depth of roller engagement at about 0.060 inch to 0.120 inch at speeds from about 550 fpm to 1200 fpm or faster.
  • the results of such incremental or intermesh stretching produces laminates that have excellent breathability and liquid-barrier properties, yet provide superior bond strengths and soft cloth-like textures.
  • FIG. 1 is a schematic of an inline extrusion lamination and incremental stretching apparatus for making the microporous laminate of this invention.
  • FIG. 2 is a cross sectional view taken along the line 2--2 of FIG. 1 illustrating the intermeshing rollers in diagrammatic form.
  • FIG. 3 is a graph demonstrating the line speeds for Examples 1-5.
  • FIG. 4 is a graph demonstrating the moisture vapor transmission properties of both embossed and flat microporous films.
  • FIG. 5 is a graph demonstrating the moisture vapor transmission rate can be adjusted by heating the precursor film.
  • Blends of LLDPE and LDPE having the compositions reported in the following TABLE 1 were extruded to form films and the films were then incrementally stretched to provide microporous films.
  • each of the formulations of 1-5 were extruded into films employing an extrusion apparatus as shown diagramatically in FIG. 1. As shown, the apparatus may be employed for film extrusion with and without lamination.
  • the formulations of Examples 1-5 were fed from an extruder 1 through slot die 2 to form the extrudate 6 into the nip of a rubber roll 5 and a metal roll 4 with an air knife 3.
  • extrusion lamination there is an incoming web of fibrous material 9 from roller 13 which is also introduced into the nip of the rubber roll 5 and metal roll 4.
  • the thermoplastic film was produced for subsequent incremental stretching to form the microporous film.
  • a polyethylene film 6 on the order of about 2 mils in thickness was made which is taken off at roller 7.
  • the air knife 3 has a length of about 120" and an opening of about 0.035"-0.060" and air is blown through the opening and against the extrudate 6 at about 5 cfm/inch to 25 cfm/inch.
  • the compressive force at the nip and the air knife are controlled such that the film is made without pin holing and without draw resonance in the case of Examples 2-5.
  • draw resonance was encountered at a line speed of 550 fpm.
  • FIG. 3 is a graph demonstrating the line speeds for Examples 1-5.
  • Example 1 which contained only 1.5% by weight of LDPE, resulted in a poor film gauge control with draw resonance even with the air knife 3.
  • the LDPE was increased to about 3.7% by weight, excellent web stability was achieved without draw resonance even when line speeds were increased to about 1200 fpm. This is shown diagramatically in FIG. 3.
  • FIG. 4 is a graph demonstrating the moisture vapor transmission properties of both embossed and flat films resulting from incrementally stretching the precursor films of Examples 2-5 under different temperatures and stretch roller engagement conditions.
  • the temperatures and the depths of engagements can be controlled.
  • the MVTR of the flat film exceeded the MVTR of the embossed film as shown in FIG. 4.
  • MVTRs for the embossed film on the order of about 1200-2400 gms/m 2 /day were achieved, whereas MVTRs for the flat film on the order of about 1900-3200 gms/m 2 /day were achieved.
  • the MVTR of the microporous film can also be controlled by the web temperature during the stretching.
  • FIG. 5 shows the film when heated to different temperatures before CD stretching can result in different MVTRs.
  • the data reported in FIG. 5 was for a CD rollers engagement dept of 0.065" and MD rollers engagement depth of 0.040" where the temperature of roller 21 was maintained at ambient.
  • the embossed film was made with a metal embossing roller having a rectangular engraving of CD and MD lines with about 165-300 lines per inch.
  • This pattern is disclosed, for example, in U.S. Pat. No. 4,376,147 which is incorporated herein by reference. This micro pattern provides a matte finish to the film but is undetectable to the naked eye.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Textile Engineering (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
  • Laminated Bodies (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
US09/080,063 1998-05-15 1998-05-15 High speed method of making microporous film products Expired - Lifetime US6013151A (en)

Priority Applications (25)

Application Number Priority Date Filing Date Title
US09/080,063 US6013151A (en) 1998-05-15 1998-05-15 High speed method of making microporous film products
ARP990102208A AR015777A1 (es) 1998-05-15 1999-05-11 Metodo de alta velocidad para fabricar una pelicula termoplastica microporosa y producto obtenido con dicho metodo
TW088107700A TWI239978B (en) 1998-05-15 1999-05-12 High speed method of making microporous film products
TW094108528A TWI252858B (en) 1998-05-15 1999-05-12 High speed method of making microporous film products
CZ20004041A CZ298026B6 (cs) 1998-05-15 1999-05-13 Vysokorychlostní zpusob výroby mikroporézního termoplastického filmu a film vyrobený tímto zpusobem
CN99805984A CN1300305A (zh) 1998-05-15 1999-05-13 高速制备微孔膜产品的方法
RU2000128113/04A RU2224772C2 (ru) 1998-05-15 1999-05-13 Высокоскоростной способ изготовления изделий из микропористой пленки
EP04077292A EP1482005A3 (de) 1998-05-15 1999-05-13 Hochgeschwindigkeitsverfahren zur Herstellung einer mikroporösen Folie
KR1020007012175A KR100583548B1 (ko) 1998-05-15 1999-05-13 미소 다공성 필름 생성물의 고속 제조방법
ES99923008T ES2244195T3 (es) 1998-05-15 1999-05-13 Procedimiento de alta velocidad para fabricar peliculas microporosas.
NZ507461A NZ507461A (en) 1998-05-15 1999-05-13 High speed method of making microporous film products
CA002329529A CA2329529A1 (en) 1998-05-15 1999-05-13 High speed method of making microporous film products
BR9910040-1A BR9910040A (pt) 1998-05-15 1999-05-13 Método de produção a alta velocidade de filme termoplástico microporoso e respectivo filme
JP2000549665A JP2002515367A (ja) 1998-05-15 1999-05-13 微孔質フィルム製品の高速度製造方法
HU0102654A HU226496B1 (en) 1998-05-15 1999-05-13 High speed method of making microporous film products
KR1020067001225A KR100704513B1 (ko) 1998-05-15 1999-05-13 점진적으로 신장된 엠보싱 미처리 필름
PCT/US1999/010562 WO1999060050A1 (en) 1998-05-15 1999-05-13 High speed method of making microporous film products
AU39877/99A AU739260B2 (en) 1998-05-15 1999-05-13 High speed method of making microporous film products
EP99923008A EP1078013B1 (de) 1998-05-15 1999-05-13 Hochgeschwindigkeitsverfahren zur herstellung einer mikroporösen folie
AT99923008T ATE301154T1 (de) 1998-05-15 1999-05-13 Hochgeschwindigkeitsverfahren zur herstellung einer mikroporösen folie
DE69926497T DE69926497T2 (de) 1998-05-15 1999-05-13 Hochgeschwindigkeitsverfahren zur herstellung einer mikroporösen folie
PL343906A PL201500B1 (pl) 1998-05-15 1999-05-13 Sposób szybkiego wytwarzania mikroporowatej folii termoplastycznej oraz niewytłaczana mikroporowata przyrostowo rozciągana folia o wysokim wskaźniku przepuszczalności pary wodnej
US09/480,374 US6656581B2 (en) 1998-05-15 2000-01-10 Incrementally stretched non-embossed films having high moisture vapor transmission rates (MVTRs)
US09/548,403 US20030047271A1 (en) 1998-05-15 2000-04-13 Microembossed thin microporous films having improved impact strength and high moisture vapor transmission rates (MVTRs)
NO20005689A NO20005689D0 (no) 1998-05-15 2000-11-10 Höyhastighets fremgangsmåte for fremstilling av mikroporöse filmprodukter

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US09/080,063 US6013151A (en) 1998-05-15 1998-05-15 High speed method of making microporous film products

Related Parent Applications (1)

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US09/395,627 Continuation-In-Part US20020074691A1 (en) 1998-05-15 1999-09-14 High speed method of making plastic film and nonwoven laminates

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US09/480,374 Continuation-In-Part US6656581B2 (en) 1998-05-15 2000-01-10 Incrementally stretched non-embossed films having high moisture vapor transmission rates (MVTRs)

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US (1) US6013151A (de)
EP (2) EP1482005A3 (de)
JP (1) JP2002515367A (de)
KR (2) KR100583548B1 (de)
CN (1) CN1300305A (de)
AR (1) AR015777A1 (de)
AT (1) ATE301154T1 (de)
AU (1) AU739260B2 (de)
BR (1) BR9910040A (de)
CA (1) CA2329529A1 (de)
CZ (1) CZ298026B6 (de)
DE (1) DE69926497T2 (de)
ES (1) ES2244195T3 (de)
HU (1) HU226496B1 (de)
NO (1) NO20005689D0 (de)
NZ (1) NZ507461A (de)
PL (1) PL201500B1 (de)
RU (1) RU2224772C2 (de)
TW (2) TWI252858B (de)
WO (1) WO1999060050A1 (de)

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EP1482005A2 (de) 2004-12-01
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AU739260B2 (en) 2001-10-11
PL201500B1 (pl) 2009-04-30
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HU226496B1 (en) 2009-03-02
EP1482005A3 (de) 2005-03-09
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JP2002515367A (ja) 2002-05-28
CZ298026B6 (cs) 2007-05-30
CA2329529A1 (en) 1999-11-25
HUP0102654A2 (hu) 2001-11-28
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ATE301154T1 (de) 2005-08-15
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BR9910040A (pt) 2001-01-02

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